EP0319064B1 - Process for the preparation of a water and oil emulsion - Google Patents
Process for the preparation of a water and oil emulsion Download PDFInfo
- Publication number
- EP0319064B1 EP0319064B1 EP19880202547 EP88202547A EP0319064B1 EP 0319064 B1 EP0319064 B1 EP 0319064B1 EP 19880202547 EP19880202547 EP 19880202547 EP 88202547 A EP88202547 A EP 88202547A EP 0319064 B1 EP0319064 B1 EP 0319064B1
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- EP
- European Patent Office
- Prior art keywords
- process according
- oil
- phospholipase
- phospholipoprotein
- emulsion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
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- 238000000034 method Methods 0.000 title claims description 34
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- 102000015439 Phospholipases Human genes 0.000 claims description 28
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- WTJKGGKOPKCXLL-RRHRGVEJSA-N phosphatidylcholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCCCCCCC=CCCCCCCCC WTJKGGKOPKCXLL-RRHRGVEJSA-N 0.000 claims description 8
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- 239000002253 acid Substances 0.000 claims description 4
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 claims description 4
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- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims description 4
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- 150000007513 acids Chemical class 0.000 claims description 3
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- 229920006395 saturated elastomer Polymers 0.000 claims description 2
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- 239000003921 oil Substances 0.000 description 31
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- 102000004190 Enzymes Human genes 0.000 description 2
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- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
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- 239000000084 colloidal system Substances 0.000 description 2
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- 229940088598 enzyme Drugs 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 235000008216 herbs Nutrition 0.000 description 2
- 239000004615 ingredient Substances 0.000 description 2
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- 150000003904 phospholipids Chemical class 0.000 description 2
- 235000002639 sodium chloride Nutrition 0.000 description 2
- 235000012424 soybean oil Nutrition 0.000 description 2
- 239000003549 soybean oil Substances 0.000 description 2
- 235000013599 spices Nutrition 0.000 description 2
- 244000056139 Brassica cretica Species 0.000 description 1
- 235000003351 Brassica cretica Nutrition 0.000 description 1
- 235000003343 Brassica rupestris Nutrition 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000005979 Citrus limon Nutrition 0.000 description 1
- 244000131522 Citrus pyriformis Species 0.000 description 1
- 239000004150 EU approved colour Substances 0.000 description 1
- 229920000161 Locust bean gum Polymers 0.000 description 1
- 102000014171 Milk Proteins Human genes 0.000 description 1
- 108010011756 Milk Proteins Proteins 0.000 description 1
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- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 239000005862 Whey Substances 0.000 description 1
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- 230000002378 acidificating effect Effects 0.000 description 1
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- QKSKPIVNLNLAAV-UHFFFAOYSA-N bis(2-chloroethyl) sulfide Chemical compound ClCCSCCCl QKSKPIVNLNLAAV-UHFFFAOYSA-N 0.000 description 1
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- 238000003776 cleavage reaction Methods 0.000 description 1
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- 235000003599 food sweetener Nutrition 0.000 description 1
- 235000011389 fruit/vegetable juice Nutrition 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- PEDCQBHIVMGVHV-UHFFFAOYSA-N glycerol group Chemical group OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000000711 locust bean gum Substances 0.000 description 1
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- 244000005700 microbiome Species 0.000 description 1
- 235000021239 milk protein Nutrition 0.000 description 1
- 235000010460 mustard Nutrition 0.000 description 1
- 229940006093 opthalmologic coloring agent diagnostic Drugs 0.000 description 1
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- 235000014347 soups Nutrition 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
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- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 1
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Images
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23D—EDIBLE OILS OR FATS, e.g. MARGARINES, SHORTENINGS OR COOKING OILS
- A23D7/00—Edible oil or fat compositions containing an aqueous phase, e.g. margarines
- A23D7/005—Edible oil or fat compositions containing an aqueous phase, e.g. margarines characterised by ingredients other than fatty acid triglycerides
- A23D7/0053—Compositions other than spreads
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L15/00—Egg products; Preparation or treatment thereof
- A23L15/25—Addition or treatment with microorganisms or enzymes
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L27/00—Spices; Flavouring agents or condiments; Artificial sweetening agents; Table salts; Dietetic salt substitutes; Preparation or treatment thereof
- A23L27/60—Salad dressings; Mayonnaise; Ketchup
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
- A23L29/20—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
- A23L29/206—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
- A23L29/212—Starch; Modified starch; Starch derivatives, e.g. esters or ethers
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
- A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
- A23L33/24—Cellulose or derivatives thereof
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES, NOT OTHERWISE PROVIDED FOR; PREPARATION OR TREATMENT THEREOF
- A23L35/00—Foods or foodstuffs not provided for in groups A23L5/00 - A23L33/00; Preparation or treatment thereof
- A23L35/10—Emulsified foodstuffs
Definitions
- the present invention relates to a process for the preparation of a water and oil emulsion comprising a phospholipoprotein containing material, which has been modified by phospholipase A, and at least one native starch based thickening agent. More particularly the invention relates to a process for the preparation of an oil-in-water emulsion of the mayonnaise, French dressing or salad dressing type.
- thickeners usually are chemically modified starches, which however are expensive and moreover there is an increasing demand to have these chemically modified starches replaced by native starches.
- native starches entails a number of difficulties, however, because they are more sensitive to temperature, time and shear conditions during gelatinization.
- gel formation thickening
- water separation thin film separation
- the present invention therefore relates to a process for the preparation of a water and oil emulsion comprising a phospholipoprotein containing material, which has been modified by phospholipase A, and at least one native starch based thickening agent, which comprises:
- the emulsions prepared according to the invention preferably have the aqueous phase as the continuous phase and are in this specification referred to as oil-in-water emulsions.
- This type of emulsion means for the purpose of this specification continuous aqueous phases containing any amount of oil and fat containing oil in dispersed form.
- Examples of emulsions which come under this definition are edible products like mayonnaise, dressings, spreads, soups or sauces.
- the emulsions are prepared by incorporating in the emulsion besides oil, water and modified phospholipoprotein, at least one thickening agent in a proportion, which is less than the proportion required for obtaining an emulsion of the same composition and viscosity, but containing unmodified or insufficiently modified phospholipoprotein.
- all the ingredients are mixed together in one vessel and from this publication it cannot be concluded that a specific sequence of operations in the preparation of the emulsion is necessary to arrive at an acceptable product not exhibiting water separation upon storage.
- Preferred oil-in-water emulsions are emulsions containing from 5% to 85%, more preferably from 15 to 50% of oil or fat-containing oil.
- fat we mean a triglyceride which is hard at room temperature (typically 15-25°C).
- oil-in-water emulsions can be prepared which are also stable at refrigeration temperature (4° - 10°C) using non-winterized oils.
- stable products can be prepared starting from a mixture of oil and hard fat in an amount (dependent on the type of the hard fat) of up to about 15% solid fat (based on the total oil phase) in the oil phase at 5°C.
- the oil and the fat may be of vegetable or animal origin and may be synthetic oil and fat. It may be a single oil or fat or fat fraction or a mixture of oils or fats and/or fat fractions. At least part of the oil and/or at least part of the fat may be replaced by a liquid or solid fat-replacer respectively.
- Particularly suitable fat replacers are the edible polyesters of polyhydric alcohols having at least four free hydroxyl groups, such as polyglycerols, sugar or sugar alcohols, and saturated or unsaturated, straight or branched alkyl chain C8-C24 fatty acids.
- the polyhydric alcohol fatty acid polyesters include any such polyesters or mixtures thereof of which, on average, at least 70% of the polyhydric alcohol hydroxyl groups have been esterified with the fatty acids. Also fatty alkyl ether derivatives of glycerol, esters of C8-C24 fatty alcohols and polycarboxylic acids, waxes and microcrystalline cellulose can be used for replacing at least part of the oil or the fat.
- phospholipoprotein-containing materials are skim milk, butter milk, whey, cream, egg yolk and whole egg.
- Egg yolk is used preferably as source of the phospholipoprotein.
- Egg yolk or other sources of phospholipoprotein can be subjected to the action of phospholipase A, particularly phospholipase A2 and the modified product is then incorporated in the emulsions according to the invention according to the process of this invention.
- modified applied to phospholipoprotein as used herein denotes any degree of conversion brought about by the action of phospholipase A.
- Phospholipase A is an enzyme which affects cleavage of the bond which binds a fatty acid radical to the glycerol part of the phospholipid molecule, thereby replacing this fatty acid radical by a hydroxyl group, which is called conversion.
- Phospholipase A is also active when the phospholipid is complexed with protein (and then called phospholipoprotein in this specification).
- a suitable source of phospholipase A is pancreatin which is preferably heat-treated, preferably under acidic conditions. The heat treatment is carried out at a temperature from 60°C to 90°C for 3-15 minutes preferably at pH from 4 to 6.5.
- the enzyme composition thus obtained is substantially free from enzymatic activity other than that resulting from phospholipase A, which is remarkably stable under the conditions of the above treatment.
- the degree of conversion of modified phospholipoprotein is in this specification expressed as the percentage of converted phosphatidylcholine plus phosphatidylethanolamine based on the total amount of phosphatidylcholine plus phosphatidylethanolamine present before conversion.
- An easy method to obtain the figures required to compute this percentage is quantitative thin-layer chromatography.
- Even a very low degree of conversion contributes to the emulsifying capacity of the phospholipoprotein modified by phospholipase A as well as to the heat stability of the emulsion containing it.
- the presence of unmodified phospholipoprotein is detrimental to the beneficial effects of the modified composition, without, however, totally off-setting these.
- emulsions according to the invention are emulsions, in which the degree of conversion of the phospholipoprotein, modified by phospholipase A, contained therein is from 40% to 86%, especially from 40% to 65%.
- the quantity of modified phospholipoprotein which should be present in the emulsion can vary within very wide limits. This quantity is inter alia dependent on the composition of the emulsion, the presence of other emulsifying agents, the degree of conversion of the phospholipoprotein modified by phospholipase A and the properties which are desired in the stabilized emulsion.
- the emulsions contain from 0.05% to 5% of the phospholipoprotein modified by phospholipase A based on the oil (or fat-containing oil) content of the emulsion.
- emulsions are provided containing modified egg yolk which is free of cholesterol.
- the native starch based thickening agent preferably is a hot water soluble native starch, like corn starch, wheat starch, potato starch and the like, or a mixture of said starches. Also cold-water soluble starches may be used, which usually are pregelatinized.
- the first step of the process i.e.gelatinising the native starch based thickening agent may be superfluous and in that case the phospholipoprotein containing material, which has been modified by phospholipase A, can be incorporated immediately into the pregelatinized native starch based thickening agent (process step (b)), after which the other process steps (c) and (d) according to the present invention are performed.
- process step (b) the phospholipoprotein containing material, which has been modified by phospholipase A
- process step (b) the phospholipoprotein containing material, which has been modified by phospholipase A
- the other process steps (c) and (d) according to the present invention are performed.
- from 0.1% to 10% by weight of the final emulsion of native starch based thickening agent is used, optionally conjointly with from 0.05% to 1% by weight of at least one gum, like guar gum, locust bean gum, and the like.
- the hot-water soluble native starch based thickening agent is first subjected to a gelatinising treatment by heating it to a temperature between 75°C and 90°C in the presence of water, the temperature being dependent on the type of the thickening agent used, the pH and the presence of any other additives.
- the hot-water soluble native starch based thickening agent may subsequently be cooled, but it may also be transferred in hot state to a mixing vessel, during which transfer a small temperature drop may occur.
- the hot-water soluble native starch based thickening agent before gelatinising and, optionally cooling may have been mixed with vinegar, salt, sugar, vegetables, herbs, spices and the like.
- the phospholipoprotein containing material which has been modified by phospholipase A, is incorporated into the gelatinised native starch based thickening agent. This is followed by incorporating the required amount of oil or fat containing oil, and any other ingredients of the emulsion, after which the final mixture obtained is homogenized.
- the emulsions to be prepared according to the present invention may also comprise vinegar, lime or lemon juice, edible acids, up to 6% by weight (based on the total emulsion) of ethanol, sweetening agents, salt, mustard, herbs, spices, flavouring agents, vegetable particles, emulsifying agents, colouring agents, gums and stabilizers, but the amount and the type of these additives should be such that the obtained emulsions will be mild and substantially preservative-free.
- the invention is illustrated by the following examples.
- a salad dressing having the following composition (in weight percentages): Soybean oil 35.0% Modified egg yolk 4.5% Vinegar (7.5%) 4.5% Native wheat starch 5.6% Guar gum 0.1% Sugar 1.75% Salt 0.5% Water 48.05% in which the egg yolk was modified with phospholipase A to a degree of conversion of 70%, was prepared by gelatinising the native wheat starch together with the guar gum, the salt, the sugar, the vinegar and the water by heating these components together to 85°C under gentle stirring.
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- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Nutrition Science (AREA)
- Health & Medical Sciences (AREA)
- Microbiology (AREA)
- Mycology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Dispersion Chemistry (AREA)
- Seasonings (AREA)
- Edible Oils And Fats (AREA)
- Coloring Foods And Improving Nutritive Qualities (AREA)
Description
- The present invention relates to a process for the preparation of a water and oil emulsion comprising a phospholipoprotein containing material, which has been modified by phospholipase A, and at least one native starch based thickening agent. More particularly the invention relates to a process for the preparation of an oil-in-water emulsion of the mayonnaise, French dressing or salad dressing type.
- There is an increasing demand for milder, preservative-free oil-in-water emulsion based products, which have not been subjected to severe heat treatments, but at the same time have an acceptable taste and good keeping properties. In order to prepare these products, the manufacturer faces a number of sometimes conflicting requirements. If the product has to be mild, the use of chemical preservatives to inhibit the growth of unacceptable microorganisms is almost unavoidable. If on the other hand the product should be free of these chemical preservatives, one has to resort to the use of such amounts of acid in order to arrive at an acceptable shelf life of the product, that the taste of the product is unacceptably harsh.
Mild products, which are fee of chemical preservatives usually require a pasteurization or sterilization treatment, but upon heating above 60°C-70°C the egg yolk in oil-in-water emulsions looses its emulsifying properties, which results in coarsening of the emulsion, followed by oil exudation. Products based on milk protein instead of egg yolk as emulsifying agent are generally heat-stable at 60°C-70°C, but lack the desired creamy taste impression originating from the egg yolk. With salad dressing an additional problem is met. Salad dressing resembles mayonnaise in that it is also an oil-in-water emulsion, but in addition to egg yolk it contains starch based thickening agents and gums. These thickeners usually are chemically modified starches, which however are expensive and moreover there is an increasing demand to have these chemically modified starches replaced by native starches. The use of native starches entails a number of difficulties, however, because they are more sensitive to temperature, time and shear conditions during gelatinization. Moreover during storage of the dressings prepared with native starches, gel formation (thickening) and as a consequence water separation (syneresis) often occurs due to retrogradation of the starch, leading to unacceptable products. - It has now been found that these disadvantages can be overcome by using a phospholipoprotein containing material, which has been modified by phospholipase A, and preparing the oil and water emulsion containing at least one native starch based thickening agent by using a specific sequence of operations.
- The present invention therefore relates to a process for the preparation of a water and oil emulsion comprising a phospholipoprotein containing material, which has been modified by phospholipase A, and at least one native starch based thickening agent, which comprises:
- (a) at least partially gelatinising the native starch based thickening agent,
- (b) incorporating the phospholipoprotein containing material, which has been modified by phospholipase A, into the gelatinised native starch based thickening agent,
- (c) incorporating from 5% to 85% by weight of oil or fat containing oil into the mixture obtained in step (b), and
- (d) homogenizing the final mixture obtained.
- The emulsions prepared according to the invention preferably have the aqueous phase as the continuous phase and are in this specification referred to as oil-in-water emulsions. This type of emulsion means for the purpose of this specification continuous aqueous phases containing any amount of oil and fat containing oil in dispersed form. Examples of emulsions which come under this definition are edible products like mayonnaise, dressings, spreads, soups or sauces.
- It is known from British Patent Specification 1,585,105 (Unilever) to prepare oil-in-water emulsions comprising hot- and cold-water-soluble, optionally modified, kinds of starch and gums and a phospholipoprotein material, modified by a treatment with phospholipase A. This publication is silent, however, on the occurrence of water separation of the products upon storage and with regard to the preparation of the emulsions it has only been stated that the emulsions are prepared by incorporating in the emulsion besides oil, water and modified phospholipoprotein, at least one thickening agent in a proportion, which is less than the proportion required for obtaining an emulsion of the same composition and viscosity, but containing unmodified or insufficiently modified phospholipoprotein. In the examples all the ingredients are mixed together in one vessel and from this publication it cannot be concluded that a specific sequence of operations in the preparation of the emulsion is necessary to arrive at an acceptable product not exhibiting water separation upon storage.
- Preferred oil-in-water emulsions are emulsions containing from 5% to 85%, more preferably from 15 to 50% of oil or fat-containing oil. By fat we mean a triglyceride which is hard at room temperature (typically 15-25°C). With the process according to the invention oil-in-water emulsions can be prepared which are also stable at refrigeration temperature (4° - 10°C) using non-winterized oils. In general stable products can be prepared starting from a mixture of oil and hard fat in an amount (dependent on the type of the hard fat) of up to about 15% solid fat (based on the total oil phase) in the oil phase at 5°C.
- The oil and the fat may be of vegetable or animal origin and may be synthetic oil and fat. It may be a single oil or fat or fat fraction or a mixture of oils or fats and/or fat fractions.
At least part of the oil and/or at least part of the fat may be replaced by a liquid or solid fat-replacer respectively. Particularly suitable fat replacers are the edible polyesters of polyhydric alcohols having at least four free hydroxyl groups, such as polyglycerols, sugar or sugar alcohols, and saturated or unsaturated, straight or branched alkyl chain C₈-C₂₄ fatty acids. The polyhydric alcohol fatty acid polyesters include any such polyesters or mixtures thereof of which, on average, at least 70% of the polyhydric alcohol hydroxyl groups have been esterified with the fatty acids. Also fatty alkyl ether derivatives of glycerol, esters of C₈-C₂₄ fatty alcohols and polycarboxylic acids, waxes and microcrystalline cellulose can be used for replacing at least part of the oil or the fat. - Examples of phospholipoprotein-containing materials are skim milk, butter milk, whey, cream, egg yolk and whole egg. Egg yolk is used preferably as source of the phospholipoprotein.
- Egg yolk or other sources of phospholipoprotein can be subjected to the action of phospholipase A, particularly phospholipase A₂ and the modified product is then incorporated in the emulsions according to the invention according to the process of this invention.
The expression "modified" applied to phospholipoprotein as used herein denotes any degree of conversion brought about by the action of phospholipase A. Phospholipase A is an enzyme which affects cleavage of the bond which binds a fatty acid radical to the glycerol part of the phospholipid molecule, thereby replacing this fatty acid radical by a hydroxyl group, which is called conversion. Phospholipase A is also active when the phospholipid is complexed with protein (and then called phospholipoprotein in this specification).
A suitable source of phospholipase A is pancreatin which is preferably heat-treated, preferably under acidic conditions. The heat treatment is carried out at a temperature from 60°C to 90°C for 3-15 minutes preferably at pH from 4 to 6.5. The enzyme composition thus obtained is substantially free from enzymatic activity other than that resulting from phospholipase A, which is remarkably stable under the conditions of the above treatment.
The degree of conversion of modified phospholipoprotein is in this specification expressed as the percentage of converted phosphatidylcholine plus phosphatidylethanolamine based on the total amount of phosphatidylcholine plus phosphatidylethanolamine present before conversion. An easy method to obtain the figures required to compute this percentage is quantitative thin-layer chromatography.
Even a very low degree of conversion contributes to the emulsifying capacity of the phospholipoprotein modified by phospholipase A as well as to the heat stability of the emulsion containing it. The presence of unmodified phospholipoprotein is detrimental to the beneficial effects of the modified composition, without, however, totally off-setting these. Thus one would normally expect that replacing in an emulsion the entire modified phospholipoprotein content having a degree of conversion of, for example 40% by an equivalent amount of equal parts of unmodified phospholipoprotein and modified phospholipoprotein having a degree of conversion of 80%, would make no difference in the properties of the emulsion. It has been found, however, that the latter emulsion is appreciably less heat-stable than the former, although the latter emulsion is also appreciably better in this respect than an emulsion stabilized by an equivalent amount of unmodified phospholipoprotein.
The degree of conversion should at least be 10%. Preferred emulsions according to the invention are emulsions, in which the degree of conversion of the phospholipoprotein, modified by phospholipase A, contained therein is from 40% to 86%, especially from 40% to 65%. - The quantity of modified phospholipoprotein which should be present in the emulsion can vary within very wide limits. This quantity is inter alia dependent on the composition of the emulsion, the presence of other emulsifying agents, the degree of conversion of the phospholipoprotein modified by phospholipase A and the properties which are desired in the stabilized emulsion. In the present invention the emulsions contain from 0.05% to 5% of the phospholipoprotein modified by phospholipase A based on the oil (or fat-containing oil) content of the emulsion.
In a particular embodiment of the present invention emulsions are provided containing modified egg yolk which is free of cholesterol. - In the emulsions to be prepared according to the present invention the native starch based thickening agent preferably is a hot water soluble native starch, like corn starch, wheat starch, potato starch and the like, or a mixture of said starches. Also cold-water soluble starches may be used, which usually are pregelatinized. In case cold-water soluble starches are used in the process according to the present invention, the first step of the process, i.e.gelatinising the native starch based thickening agent may be superfluous and in that case the phospholipoprotein containing material, which has been modified by phospholipase A, can be incorporated immediately into the pregelatinized native starch based thickening agent (process step (b)), after which the other process steps (c) and (d) according to the present invention are performed.
Generally from 0.1% to 10% by weight of the final emulsion of native starch based thickening agent is used, optionally conjointly with from 0.05% to 1% by weight of at least one gum, like guar gum, locust bean gum, and the like.
In the process according to the present invention the sequence of process steps is essential to arrive at shelf-stable products.
The hot-water soluble native starch based thickening agent is first subjected to a gelatinising treatment by heating it to a temperature between 75°C and 90°C in the presence of water, the temperature being dependent on the type of the thickening agent used, the pH and the presence of any other additives.
The hot-water soluble native starch based thickening agent may subsequently be cooled, but it may also be transferred in hot state to a mixing vessel, during which transfer a small temperature drop may occur. The hot-water soluble native starch based thickening agent before gelatinising and, optionally cooling may have been mixed with vinegar, salt, sugar, vegetables, herbs, spices and the like. - Then the phospholipoprotein containing material, which has been modified by phospholipase A, is incorporated into the gelatinised native starch based thickening agent. This is followed by incorporating the required amount of oil or fat containing oil, and any other ingredients of the emulsion, after which the final mixture obtained is homogenized.
- The emulsions to be prepared according to the present invention may also comprise vinegar, lime or lemon juice, edible acids, up to 6% by weight (based on the total emulsion) of ethanol, sweetening agents, salt, mustard, herbs, spices, flavouring agents, vegetable particles, emulsifying agents, colouring agents, gums and stabilizers, but the amount and the type of these additives should be such that the obtained emulsions will be mild and substantially preservative-free. The invention is illustrated by the following examples.
- A salad dressing having the following composition (in weight percentages):
Soybean oil 25.0 Modified egg yolk 2.5 Vinegar (10%) 6.7 Native maize starch 3.5 Sugar 5.5 Salt 1.92 Water 54.88
in which the egg yolk was modified with phospholipase A to a degree of conversion of 80%, was prepared in two ways: - (A) The maize starch was gelatinised by heating to 90°C with the water, sugar and salt under gentle stirring and after a holding time of 10 minutes the starch phase was cooled down to 25°C. Subsequently the vinegar, the modified egg yolk and the oil were added (in this sequence) while stirring and the obtained mixture was homogenised in a colloid mill.
- (B) After having prepared the cooled starch phase as under (A) the vinegar, the modified egg yolk and the oil were mixed and the mixture was separately emulsified and homogenised. This homogenised emulsion of vinegar, modified egg yolk and oil was subsequently mixed with the cooled starch phase.
- The samples of product as prepared via route (A) and via route (B) were stored at 15°C and visually assessed for their storage stability, particularly paying attention to gel formation (so-called after-gelling) and water separation. The texture of the products was measured with the Stevens Texture Analyser (using grid no.6, speed 1 mm/sec and penetration depth 2.5 cm). The results of the texture investigation have been depicted in Figure 1. In this figure also the behaviour of the texture upon storage of a similar product has been depicted, which product had the same composition, the modified egg yolk, however, being replaced by normal native egg yolk. For the preparation of this product also route (A) was followed.
- In the product samples prepared via route (A), which is according to the process of the present invention, no visual product instability was observed during storage (up to 4 months), but it was observed that with the products prepared via route (B) the instability could only be delayed for a few weeks. After this period after-gelling started, later followed by water separation.
- The product with normal, non-modified egg yolk prepared by the process according to the present invention showed after-gelling within a short time, later followed by water separation.
These results clearly demonstrate that only if the heat processed and cooled native starch based thickening agent is first mixed with the egg yolk, modified by treatment with phospholipase A, followed by the addition of the oil or the oil containing fat, an ambient stable pourable salad dressing with a creamy taste could be obtained. - A salad dressing having the following composition (in weight percentages):
Soybean oil 35.0% Modified egg yolk 4.5% Vinegar (7.5%) 4.5% Native wheat starch 5.6% Guar gum 0.1% Sugar 1.75% Salt 0.5% Water 48.05%
in which the egg yolk was modified with phospholipase A to a degree of conversion of 70%, was prepared by gelatinising the native wheat starch together with the guar gum, the salt, the sugar, the vinegar and the water by heating these components together to 85°C under gentle stirring. The mixture obtained washold 10 minutes at 85°C under stirring and was subsequently pumped to a mixing vessel in which it was mixed under stirring with the modified egg yolk and finally the oil was added and the final mixture was homogenized in a colloid mill, upon which a mild dressing (pH = 4.1) without preservatives was obtained, which after filling into glass jars and upon storage at 15°C for 12 months showed no after-gelling or water separation and had a constant Stevens value of 20-22 (measured under the same conditions as in Example I).
Claims (19)
- A process for the preparation of a water and oil emulsion comprising a phospholipoprotein containing material, which has been modified by phospholipase A, and at least one native starch based thickening agent, which comprises:(a) at least partly gelatinizing the native starch based thickening agent,(b) incorporating the phospholipoprotein containing material, which has been modified by phospholipase A, into the gelatinized native starch based thickening agent,(c) incorporating from 5% to 85% by weight of oil or fat containing oil into the mixture obtained in step (b) and,(d) homogenizing the final mixture obtained.
- A process according to claim 1, in which the emulsion is an oil-in-water emulsion.
- A process according to claim 1 or 2, in which the phospholipoprotein containing material is selected from: whole egg, egg yolk, or egg yolk free from cholesterol.
- A process according to claims 1-3, in which all of the phospholipoprotein has been subjected to the treatment with phospholipase A.
- A process according to claims 1-4, in which from 0.05% to 5% by weight, based on the oil content of the emulsion, of phospholipoprotein, modified by phospholipase A, is present.
- A process according to claims 1-5, in which the degree of conversion expressed as the percentage of converted phosphatidylcholine plus phosphatidylethanolamine based on the total amount of phosphatidylcholine plus phosphatidylethanolamine present before conversion of the phospholipoprotein by the phospholipase A as used therein is at least 10%.
- A process according to claims 1-5, in which the degree of conversion expressed as the percentage of converted phosphatidylcholine plus phosphatidylethanolamine based on the total amount of phosphatidylcholine plus phosphatidylethanolamine present before conversion of the phospholipoprotein by the phospholipase A is from 40% to 86%
- A process according to claims 1-5, in which the degree of conversion expressed as the percentage of converted phosphatidylcholine plus phosphatidylethanolamine based on the total amount of phosphatidylcholine plus phosphatidylethanolamine present before conversion of the phospholipoprotein by the phospholipase A is from 40% to 65%.
- A process according to claims 1-8, in which the phospholipase A is phospholipase A2.
- A process according to claims 1-9, in which from 15% to 50% by weight of oil is used.
- A process according to claims 1-10, in which up to 15% of hard fat is used, based on the weight of the oil phase of the emulsion.
- A process according to claims 1-11, in which at least part of the oil is replaced by a liquid fat replacer.
- A process according to claim 11, in which at least part of the hard fat is replaced by a solid fat replacer.
- A process according to claims 12 and 13, in which the fat-replacer is selected from the group consisting of: polyesters of polyhydric alcohols having at least four free hydroxyl groups of which on an average at least 70% have been esterified with saturated or unsaturated, straight or branched alkyl chain C₈-C₂₄ fatty acids, fatty alkyl ether derivatives of glycerol; esters of C₈-C₂₄ fatty alcohols and polycarboxylic acids; waxes; microcrystalline cellulose, or mixtures thereof.
- A process according to claims 1-14, in which the native starch based thickening agent is a hot-water soluble native starch selected from the group consisting of corn starch, wheat starch, potato starch, and mixtures thereof.
- A process according to claims 1-15, in which from 0.1% to 10% by weight of the final emulsion of native starch thickening agent is used.
- A process according to claims 1-16, in which from 0.05% to 1% by weight of the final emulsion of at least one gum is used.
- A process according to claim 17, in which the gum is guar gum.
- A process according to claims 1-18, in which the native starch based thickening agent is step (a) is gelatinized by heating to a temperature between 75°C and 90°C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT88202547T ATE75919T1 (en) | 1987-12-03 | 1988-11-15 | PROCESS FOR PREPARING A WATER-IN-OIL EMULSION. |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP87202399 | 1987-12-03 | ||
EP87202399 | 1987-12-03 | ||
EP88202144 | 1988-09-30 | ||
EP88202144 | 1988-09-30 |
Publications (3)
Publication Number | Publication Date |
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EP0319064A2 EP0319064A2 (en) | 1989-06-07 |
EP0319064A3 EP0319064A3 (en) | 1989-08-23 |
EP0319064B1 true EP0319064B1 (en) | 1992-05-13 |
Family
ID=26109479
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19880202547 Expired - Lifetime EP0319064B1 (en) | 1987-12-03 | 1988-11-15 | Process for the preparation of a water and oil emulsion |
Country Status (9)
Country | Link |
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US (1) | US5028447A (en) |
EP (1) | EP0319064B1 (en) |
JP (1) | JPH01199559A (en) |
AU (1) | AU598703B2 (en) |
CA (1) | CA1310224C (en) |
DE (1) | DE3871095D1 (en) |
ES (1) | ES2032000T3 (en) |
GR (1) | GR3005049T3 (en) |
PH (1) | PH25356A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6773731B2 (en) | 2002-10-18 | 2004-08-10 | James S. Campbell | Liquid egg yolk product comprising lysophospholipoprotein |
Families Citing this family (40)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
AR244514A1 (en) * | 1989-01-25 | 1993-11-30 | Cpc International Inc | Cholesterol-free salad dressing |
US5213968A (en) * | 1989-08-21 | 1993-05-25 | Nestec S.A. | Process for preparing emulsifying agents |
US5037661A (en) * | 1990-03-16 | 1991-08-06 | Kraft General Foods, Inc. | Functional decholesterolized egg yolks |
EP0546215B1 (en) * | 1991-12-12 | 1998-04-01 | Societe Des Produits Nestle S.A. | Heat stable oil-in-water emulsion and process for its preparation |
DK0628256T3 (en) * | 1993-06-11 | 1998-03-09 | Nestle Sa | Means for thermal stabilization of proteins and product obtained therefrom |
DK0716811T3 (en) * | 1994-12-13 | 2001-07-09 | Nestle Sa | Heat-stable oil-in-water emulsion containing egg yolk as well as a process for making them |
EP0810825B1 (en) * | 1995-02-22 | 2001-08-08 | Unilever Plc | High temperature cooking sauce |
US5800850A (en) * | 1995-07-07 | 1998-09-01 | Nestec S.A. | Process for reducing spoilage of sterilized liquid products |
ATE441704T1 (en) | 1998-11-27 | 2009-09-15 | Novozymes As | VARIANTS OF A LIPOLYTIC ENZYME |
EP1280919A2 (en) | 2000-04-28 | 2003-02-05 | Novozymes A/S | Lipolytic enzyme variants |
US6660312B2 (en) | 2001-04-20 | 2003-12-09 | Kewpie Kabushiki Kaisha | Egg yolk-containing, reduced-cholesterol, oil-in-water emulsified food and the preparation thereof |
AU2002336717B2 (en) * | 2001-11-06 | 2008-04-03 | Novozymes North America, Inc. | Modified whey protein compositions having improved foaming properties |
DK2295556T3 (en) | 2002-01-16 | 2015-01-26 | Novozymes As | Lipolytic Enzyme Variants and Method of Preparation thereof. |
US20040047947A1 (en) * | 2002-02-21 | 2004-03-11 | Scott Bloomer | Method of preparing a milk polar lipid and a sphingolipid enriched concentrate |
US6863908B2 (en) * | 2002-04-25 | 2005-03-08 | Unilever Bestfoods, North America Division Of Conopco Inc. | Universal sauce base |
US7309510B2 (en) * | 2003-02-28 | 2007-12-18 | Unilever Bestfoods, North America Division Of Conopco, Inc. | Stable cheese condiment |
US20050136165A1 (en) * | 2003-12-23 | 2005-06-23 | Unilever Bestfoods, North America | Flavor and microbiologically stable food composition |
US20050169970A1 (en) | 2004-02-02 | 2005-08-04 | Unilever Bestfoods, North America | Food composition with fibers |
CA2587488A1 (en) * | 2004-04-16 | 2005-10-27 | Inovatech Egg Products, A Division Of Mfi Food Canada Ltd. | Liquid egg yolk product comprising lysophospholipoprotein |
US20050244565A1 (en) * | 2004-04-29 | 2005-11-03 | Unilever Bestfoods, North America | Edible emulsion with reduced fat and cholesterol |
US20060040022A1 (en) * | 2004-08-20 | 2006-02-23 | Unilever Bestfoods, North America, Division Of Conopco, Inc. | Chilled food composition |
US20060093724A1 (en) * | 2004-11-03 | 2006-05-04 | Conopco, Inc., A Corporation Of New York D/B/A Unilever Foodsolutions | Frozen food |
US9102103B2 (en) * | 2006-02-02 | 2015-08-11 | The Boeing Company | Thermoplastic composite parts having integrated metal fittings and method of making the same |
US20070259096A1 (en) * | 2006-05-03 | 2007-11-08 | Conopco, Inc. D/B/A Unilever Foodsolutions | Frozen foodstuff |
WO2010102920A1 (en) | 2009-03-11 | 2010-09-16 | Unilever Nv | Method for preparing a fibre containing emulsion |
WO2010124975A1 (en) * | 2009-04-28 | 2010-11-04 | Dsm Ip Assets B.V. | Method of preparing an egg composition |
US20110111097A1 (en) * | 2009-10-09 | 2011-05-12 | H.J. Heinz Company | Emulsified food product |
US8642038B2 (en) | 2010-07-02 | 2014-02-04 | Rembrandt Enterprises, Inc. | Isolated egg protein and egg lipid materials, and methods for producing the same |
US8916156B2 (en) | 2010-07-02 | 2014-12-23 | Rembrandt Enterprises, Inc. | Isolated egg protein and egg lipid materials, and methods for producing the same |
US20120034353A1 (en) | 2010-08-09 | 2012-02-09 | Joerg Eggeling | High Pressure Homogenization In Combination With Functionalized Egg For Production Of Emulsion-Based Food Products |
JP5698959B2 (en) * | 2010-11-08 | 2015-04-08 | キユーピー株式会社 | A seasoning liquid for potato processed food and a potato processed food using the same. |
US20120164276A1 (en) | 2010-12-22 | 2012-06-28 | Conopco, Inc., D/B/A Unilever | Dressing |
GB201107221D0 (en) * | 2011-05-03 | 2011-06-15 | Givaudan Sa | Process |
PL2866583T3 (en) | 2012-06-27 | 2017-08-31 | Unilever N.V. | Edible oil-in-water emulsion |
WO2014001030A1 (en) | 2012-06-27 | 2014-01-03 | Unilever N.V. | Edible oil-in-water emulsion |
US20170042207A1 (en) * | 2014-05-06 | 2017-02-16 | Conopco, Inc., D/B/A Unilever | Composition in the form of an oil-in-water emulsion comprising ground white or yellow mustard seed |
EP3373746B1 (en) | 2015-11-13 | 2019-09-04 | Unilever NV | Process for the manufacture of an aqueous dispersion comprising mustard bran and oil-in-water emulsion containing such dispersion |
US12022847B2 (en) | 2017-06-26 | 2024-07-02 | Michael Foods, Inc. | Methods of egg yolk fractionation |
EP4114199A1 (en) * | 2020-03-02 | 2023-01-11 | CORN Products Development Inc. | Pulse protein emulsifiers |
EP4291036A4 (en) * | 2021-03-08 | 2024-04-03 | Fable Holdings Pty Ltd | Native-whole-starch-based fat replacer |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1525929A (en) * | 1974-11-25 | 1978-09-27 | Unilever Ltd | Stabilised emulsions comprising phospholipoprotein |
GB1585105A (en) * | 1976-04-29 | 1981-02-25 | Unilever Ltd | Emulsions |
US4107335A (en) * | 1977-04-08 | 1978-08-15 | The United States Of America As Represented By The Secretary Of The Army | Freeze-dried mix for spoonable salad dressing and method therefor |
US4368213A (en) * | 1981-06-23 | 1983-01-11 | The Procter & Gamble Company | Emulsion concentrate for palatable polyester beverage |
CA1208068A (en) * | 1983-02-07 | 1986-07-22 | Richard E. Rudin | Coated pregelatinized starch and process for producing the same |
DE3423699C1 (en) * | 1984-06-27 | 1986-01-16 | Maggi AG, Kempttal | Sauce improver in tubes |
JPH0622461B2 (en) * | 1985-07-31 | 1994-03-30 | キユーピー株式会社 | Method for producing oil-in-water emulsified food |
-
1988
- 1988-11-15 EP EP19880202547 patent/EP0319064B1/en not_active Expired - Lifetime
- 1988-11-15 ES ES198888202547T patent/ES2032000T3/en not_active Expired - Lifetime
- 1988-11-15 DE DE8888202547T patent/DE3871095D1/en not_active Revoked
- 1988-11-25 JP JP63298010A patent/JPH01199559A/en active Granted
- 1988-11-30 AU AU26389/88A patent/AU598703B2/en not_active Ceased
- 1988-11-30 CA CA000584561A patent/CA1310224C/en not_active Expired - Fee Related
- 1988-12-01 PH PH37877A patent/PH25356A/en unknown
-
1990
- 1990-08-21 US US07/571,005 patent/US5028447A/en not_active Expired - Lifetime
-
1992
- 1992-06-29 GR GR920401377T patent/GR3005049T3/el unknown
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6773731B2 (en) | 2002-10-18 | 2004-08-10 | James S. Campbell | Liquid egg yolk product comprising lysophospholipoprotein |
Also Published As
Publication number | Publication date |
---|---|
EP0319064A2 (en) | 1989-06-07 |
US5028447A (en) | 1991-07-02 |
ES2032000T3 (en) | 1993-01-01 |
CA1310224C (en) | 1992-11-17 |
EP0319064A3 (en) | 1989-08-23 |
PH25356A (en) | 1991-05-13 |
JPH01199559A (en) | 1989-08-10 |
GR3005049T3 (en) | 1993-05-24 |
DE3871095D1 (en) | 1992-06-17 |
AU598703B2 (en) | 1990-06-28 |
JPH0581228B2 (en) | 1993-11-11 |
AU2638988A (en) | 1989-06-08 |
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